US1202474A - Method of accelerating the deposition of solids in sewage effluents. - Google Patents

Method of accelerating the deposition of solids in sewage effluents. Download PDF

Info

Publication number
US1202474A
US1202474A US87388714A US1914873887A US1202474A US 1202474 A US1202474 A US 1202474A US 87388714 A US87388714 A US 87388714A US 1914873887 A US1914873887 A US 1914873887A US 1202474 A US1202474 A US 1202474A
Authority
US
United States
Prior art keywords
pressure
sewage
solids
deposition
accelerating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US87388714A
Inventor
Reginald Pelham Bolton
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EDMUND F TWEEDY
Original Assignee
EDMUND F TWEEDY
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by EDMUND F TWEEDY filed Critical EDMUND F TWEEDY
Priority to US87388714A priority Critical patent/US1202474A/en
Application granted granted Critical
Publication of US1202474A publication Critical patent/US1202474A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases

Definitions

  • any aggregation of material or particle of matter suspended in the liquid is subjected to pressure in every direction, which compresses it and reduces its "displacement.
  • the particle Upon being thus reduced in size, the particle will displace less liquid and therefore be sustained by a correspondingly decreased supporting power. Consequently its descent will be accelerated in proportion to its re duction in size.
  • My complete method includes further the sudden release of the applied pressure for the purpose of detaching gases, which are attached to, or combined with, or contained in the floating materials.
  • detaching gases which are attached to, or combined with, or contained in the floating materials.
  • Materials which of themselves are heavier than water are often suspended therein by such contained or attached gases.
  • fibrous material is composed of cells containing air or gas which aids in displacing sufiicient liquid to cause the suspension of the fibrous material or to retard its deposition.
  • bubbles of gas, formed by decomposition are attached to particles of solid matter with a similar effect.
  • Such gases when subjected to severe compression are reduced to a lesser size of globule and thus afford less buoyancy to the solid. If in the form of a bubble, then compression and sudden release gives them an opportunity of releasing themselves from any particles to which they have become attached.
  • the method by which I propose to accomplish these results without the exertion of excessive energy is to utilize the flow of the sewage, by gravity, to fill a closed cylinder, receptacle, or drum, above which is a cylinder, in which is a plunger which forms a part, or an extension of a much larger piston, contained in another cylinder, superimposed on that in which theplunger works.
  • a closed cylinder, receptacle, or drum above which is a cylinder, in which is a plunger which forms a part, or an extension of a much larger piston, contained in another cylinder, superimposed on that in which theplunger works.
  • the sewage tank A and the liquid receiving tank B are not necessary parts, since the sewage may be received and the liquid discharged without the use of the tanks, but when used, A is preferably on a higher level and B on a lower level than the pressure tank.
  • the pressure apparatus consists of a cyprovided with a sewage inlet G controlled by valve G and a sludge outlet H controlled by valve H, and a liquid outlet J controlled by a valve J.
  • the chamber C is closed at a cover E having a cylindrical opening E of smaller diameter than that of cylinder C.
  • R is an orifice in the cylinder F to permit the passage of air from space F".
  • S is a steel stud or rod secured in piston K, passing through gland O in the usual manner and secured to a wire rope or chain T, passing over pulleys U and U and supporting a weight W proportioned to overbalance the weight of piston K K.
  • a gas outlet which, as shown, is composed of pipes Q Q and a controlling valve Q, (though I do not limit myself to that exact arrangement) and a pressure gage V is preferably connected to the cylinder C. With all valves closed, except valve Q, and the piston in the position shown, sewage is admitted to chamber C by opening valve G.
  • valve Q It is permitted to rise therein, expelling the air through valve Q
  • pressure water, air or steam
  • valve 0 When it reaches the under side of K valves Q and G are closed and valve 0 is opened, admitting pressure (water, air or steam) on top of piston K, which-is thereby forced down until the desired pressure is indicated by gage V.
  • a sudden release of the pressure is then efi'ected by quickly raising lever P, thus opening valve P whereby the water, steampr air can be instantly relieved and exhausted.
  • the weight will then lift the piston K and plunger K off the sewage, the gases which form in chamber 0 rise to space E and, by opening valve Q, these gases are permitted to escape either to the atmosphere or, if required, to an air pump.
  • valve J is opened and the clarified liqnor is allowed to draw-elf to tank B.
  • Valve H is then opened and the sludge withdrawn by gravity or by a pump to a suitable receptacle. After the chamber .is empty, all valves except Q are closed and the processdescribed is repeated.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Sludge (AREA)

Description

R. P. BOLTON.
METHOD OF ACCELERATING THE DEPOSITEON 0F souns IN SEWAGE EFFLUENTS.
APPLICATION FILED NOV 25.1914.
AI 2 c 0 d G Ll H 6 I a P A TTOR/VEV REGINALD PELHAM BOLTON, 015 NEW YORK, N. Y., ASSIGNOR 01E ONE-THIRD TO ARTHUR WILLIAMS AND ONE-THIRD T0 EDMUND F. TWEEDY.
METHOD OF ACGELERATING THE DEPOSITION OF SOLIDS IN SEWAGE JEFFLUEN TS.
LQUQAW T.
Specification of Letters Patent.
Patented Oct. 2d, WW6.
Application filed November 25, 1914:. Serial No. 873,887.
To all whom it may concern:
Be it known that I, REGINALD PELHAM BOLTON, a citizen of the United States of America, residing at New York, in the county and State of New York, have invented certain new and useful Improvements in Methods of Accelerating the Deposition of Solids in Sewage Eflluents, of which the following is a specification.
My invention relates to the disposal of sewage and particularly to a method of accelerating the deposition of solids in sewage efiiuents and of releasing contained gases, 'and it consists, primarily, in reducing the size of the solids by compression and expelling contained gases or detaching adhering globules, thus rendering the matter more dense and decreasing its support, so that it will more readily sink in the liquid, and secondarily, in releasing the pressure suddenly, whereby the globules or bubbles of gas are expanded or exploded so that they no longer aid in supporting the solids. I
The elimination of solid matters in sewage by mechanical screening is efiective only to a certain size of the particles of matter carried in the liquid. The larger particles and solid objects are readily arrested thus, but heretofore the elimination of the fine particles has required filtration, or a long period of gradual deposition.
Numerous attempts to solve the problem by using processes of a chemical and electrical nature have been made, the majority of which are expensive or complex or ineffective, but upon careful consideration of the cause and circumstances of the flotation of such fine materials in sewage, T have devised a method for their more rapid deposition, of a simple and effective character.
My complete method consists in the application of an intense pressure and a sudden release thereof. The pressure is exerted upon the liquid sewage. Thereby the contained particles or aggregations of matter, of a solid, fibrous or spongy character, are compressed and reduced in size and thus rendered incapable of suspension in the liquid.
Since pressure applied to a liquid confined in a closed vessel or cylinder is exerted equally upon all parts of any object therein, any aggregation of material or particle of matter suspended in the liquid, is subjected to pressure in every direction, which compresses it and reduces its "displacement. Upon being thus reduced in size, the particle will displace less liquid and therefore be sustained by a correspondingly decreased supporting power. Consequently its descent will be accelerated in proportion to its re duction in size.
My complete method includes further the sudden release of the applied pressure for the purpose of detaching gases, which are attached to, or combined with, or contained in the floating materials. Materials which of themselves are heavier than water are often suspended therein by such contained or attached gases. Thus, fibrous material is composed of cells containing air or gas which aids in displacing sufiicient liquid to cause the suspension of the fibrous material or to retard its deposition. Many times bubbles of gas, formed by decomposition, are attached to particles of solid matter with a similar effect. Such gases when subjected to severe compression are reduced to a lesser size of globule and thus afford less buoyancy to the solid. If in the form of a bubble, then compression and sudden release gives them an opportunity of releasing themselves from any particles to which they have become attached. Upon the release of the pressure, interior gases suddenly expand or explode and tear the containing material apart, and gases attached as bubbles will release themselves from the objects or materials to which they are attached. Thus, a pressure upon the water of a thousand pounds per square inch or 66 atmospheres,
which could be readily and inexpensively applied, would have the effect of reducing a globule of gas to one-sixty-sixth of its volume, in which condition the sudden release of pressure would leave it free to explode with a force due to its compressed conditions, capable of tearing asunder, with relatively severe force, any confining material, or violently detaching itself from any attachment to mechanical objects. Then, too, the form of globule or bubble of air attached to a floating object, is hemispherical, its attachment to the object being by its flattened base. Upon the application of higher hydraulic pressure, the bubble must become more and more spherical, since the pressure is equally exerted at all parts of its form. Tts contact with the object and its hold upon the object would be thus reduced in area, and,
. under increasing pressure, it would gradually release itself altogether. Now if the pressure were suddenly released, it would as suddenly explode, and be torn asunder, changingits shape and depriving it of its ability I .to hold fast to the object. The method by which I propose to accomplish these results without the exertion of excessive energy, is to utilize the flow of the sewage, by gravity, to fill a closed cylinder, receptacle, or drum, above which is a cylinder, in which is a plunger which forms a part, or an extension of a much larger piston, contained in another cylinder, superimposed on that in which theplunger works. When the chamher under the plunger is thus entirely filled,
pressure of water or of steam or of air, may
be applied to the upper side of the large piston, which imparts to the confined liquid a pressure corresponding to the difference between its larger area and that of the smaller plunger.
As water is practically incompressible, the only movement of the compressing plunger or piston which is. required, is that amount due to the proportionate volume of any air,
gas, fibrous or spongy materials contained in the sewage, so that the expenditure of energy by the movement of the piston and plunger is limited. One form of apparatus,
adapted for use in practising my aforesaid method, is shown in the accompanying drawlindrical chamber or tank C the bottom by a base D and at the top by ing which is a diagrammatic representation of the apparatus, the sewage tank A and the pressure tank being shown in section.
The sewage tank A and the liquid receiving tank B, are not necessary parts, since the sewage may be received and the liquid discharged without the use of the tanks, but when used, A is preferably on a higher level and B on a lower level than the pressure tank.
The pressure apparatus consists of a cyprovided with a sewage inlet G controlled by valve G and a sludge outlet H controlled by valve H, and a liquid outlet J controlled by a valve J. The chamber C is closed at a cover E having a cylindrical opening E of smaller diameter than that of cylinder C. Above the opening E and connected therewith by a reduced cylindrical extension F, is a larger cylinder F which with E vided with spring rings L, L and K with I a junk ring or platen K holding a cupleather packing K in place under the piston or plunger K. R is an orifice in the cylinder F to permit the passage of air from space F".
S is a steel stud or rod secured in piston K, passing through gland O in the usual manner and secured to a wire rope or chain T, passing over pulleys U and U and supporting a weight W proportioned to overbalance the weight of piston K K. Just below the face of plunger K, when at its upper limit of movement, I provide a gas outlet Which, as shown, is composed of pipes Q Q and a controlling valve Q, (though I do not limit myself to that exact arrangement) and a pressure gage V is preferably connected to the cylinder C. With all valves closed, except valve Q, and the piston in the position shown, sewage is admitted to chamber C by opening valve G. It is permitted to rise therein, expelling the air through valve Q When it reaches the under side of K valves Q and G are closed and valve 0 is opened, admitting pressure (water, air or steam) on top of piston K, which-is thereby forced down until the desired pressure is indicated by gage V. A sudden release of the pressure is then efi'ected by quickly raising lever P, thus opening valve P whereby the water, steampr air can be instantly relieved and exhausted. The weight will then lift the piston K and plunger K off the sewage, the gases which form in chamber 0 rise to space E and, by opening valve Q, these gases are permitted to escape either to the atmosphere or, if required, to an air pump. After a sufiicient time, valve J is opened and the clarified liqnor is allowed to draw-elf to tank B. Valve H is then opened and the sludge withdrawn by gravity or by a pump to a suitable receptacle. After the chamber .is empty, all valves except Q are closed and the processdescribed is repeated.
The application of pressure, as described willhave consolidated the solid, fibrous or spongy matter suspended in the liquid sewage and have compressed the globules of gas, and the sudden release of that pressure will have resulted in the described expansion or explosion of said globules and their detachment from the suspended matter thereby accelerating the deposition of said suspended matter as already set forth.- Good results may be attained by using a suitable pressure which is not suddenly released, but a much better result is reached by employing all the forces of the complete method.
' What I claim as my invention and desire to secure by Letters Patent is 1. The, method of accelerating the deposition of solids in sewage efiluents, which consists in subjecting said efiiuents to pressure eeann intermittently applying to said efiiuents, a
pressure other than that due to the depth of the liquid containing the solids to be precipitated and suflicient to condense said solids, and permitting the solids to settle, all substantially as set forth.
3. The method of accelerating the deposition of solids in sewage efiluents, which consists in placing the sewage in a vessel, closing said vessel, intermittently subjecting the 4 contents to a pressure other-than that due to the depth, above the solid, of the liquid containing the solid to be precipitated and suitable to condense said solids and then permitting them to settle, all substantially as set forth.
4. The method of accelerating the deposition of solids in sewage efiluents, which consists in placing the sewage in a vessel, closing said vessel, intermittently subjecting the contents to a pressure other than that due to the depth, above the solid, of the liquid containing the solid to be precipitated and suitable to condense said solids and to free them from gases and then permitting them to settle, all substantially as set forth.
5. The method of accelerating the deposition of solids in sewage efiiuents, which consists in placing the sewage in a vessel from which the air is permitted-to escape, closing the vessel, subjecting the contents to a pressure suitable to condense said solids, releasing the gases which separatefrom the liquid and permitting the solids to settle, all substantially as set forth.
6. The method of accelerating the deposition of solids in sewage efliuents, which consists in placing the sewage in a vessel, closing the vessel, subjecting the contents to a pressure suitable to condense said solids, relieving the pressure, releasing the gases which separate from the liquid and permitting the solids to settle, all substantially as set-forth.
In testimony whereof, I have signed my name to this specification in the presence of two subscribing witnesses, this twenty-third day of November 1914.
REGINALD PELHAM BOLTON.
Witnesses:
FREDERICK A. FORGEE, ERIC ll. BOLTON.
US87388714A 1914-11-25 1914-11-25 Method of accelerating the deposition of solids in sewage effluents. Expired - Lifetime US1202474A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US87388714A US1202474A (en) 1914-11-25 1914-11-25 Method of accelerating the deposition of solids in sewage effluents.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US87388714A US1202474A (en) 1914-11-25 1914-11-25 Method of accelerating the deposition of solids in sewage effluents.

Publications (1)

Publication Number Publication Date
US1202474A true US1202474A (en) 1916-10-24

Family

ID=3270411

Family Applications (1)

Application Number Title Priority Date Filing Date
US87388714A Expired - Lifetime US1202474A (en) 1914-11-25 1914-11-25 Method of accelerating the deposition of solids in sewage effluents.

Country Status (1)

Country Link
US (1) US1202474A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2830041A (en) * 1952-03-24 1958-04-08 Cline Mcgarvey Method for refining oleo-resinous material
US4556491A (en) * 1983-09-29 1985-12-03 Air Products And Chemicals, Inc. Avoidance of rising sludge in biological wastewater treatment clarifiers
WO2002074408A1 (en) * 2001-03-13 2002-09-26 Siemens Axiva Gmbh & Co. Kg Method and device for biological effluent treatment with integrated sludge separation by sedimentation with pressurisation

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2830041A (en) * 1952-03-24 1958-04-08 Cline Mcgarvey Method for refining oleo-resinous material
US4556491A (en) * 1983-09-29 1985-12-03 Air Products And Chemicals, Inc. Avoidance of rising sludge in biological wastewater treatment clarifiers
WO2002074408A1 (en) * 2001-03-13 2002-09-26 Siemens Axiva Gmbh & Co. Kg Method and device for biological effluent treatment with integrated sludge separation by sedimentation with pressurisation

Similar Documents

Publication Publication Date Title
US4369100A (en) Method for enhancing chemical reactions
CA2218969A1 (en) Hydraulic reactor and classifier for solid particles with ultrasonic application
US2985324A (en) Apparatus for passing particles from a high pressure vessel
GB1334248A (en) Method and apparatus for separating objects accordint to density
KR101228045B1 (en) Device and installation for injecting particulate materials into a chamber, and corresponding method
US1202474A (en) Method of accelerating the deposition of solids in sewage effluents.
EP0465242A1 (en) Method and apparatus for producing compressed air
Kuenen Settling convection and grain-size analysis
GB971658A (en) Floating separator
US3870635A (en) Apparatus for clarifying an influent water
US2854136A (en) Method and apparatus for separating solid materials of different specific gravities
US4391705A (en) Ballasting digestor covers
US1355476A (en) Method of destroying cellular structures
Lockhart Combined field dewatering: bridging the science-industry gap
JPWO2011018972A1 (en) Bubble removing method and bubble removing apparatus
CN207713597U (en) A kind of high-efficient biological reactor for ternary composite flooding water extraction processing
US2146033A (en) Handling of sensitive materials
US4961842A (en) Siphon gravity classifier and clarifier
Ebhardt Experimental compaction of carbonate sediments
EP0053094A3 (en) Method and device for separating particulate solid materials from their mixture with liquids, such as gases from such mixtures, and application of the method
Kawashima et al. Some experiments on the effect of contact angle in agglomeration from liquids
US3256000A (en) Method of treating powder
US1360703A (en) Slime-pulp thickener
US942697A (en) Sand and slime separator and classifier.
Rulkens et al. Clean-up possibilities of contaminated soil by extraction and wet classification: effect of particle size, pollutant properties and physical state of the pollutants